KR20230014992A - Slow release fertilizer using biodegradable SAP and manufacturing method thereof - Google Patents
Slow release fertilizer using biodegradable SAP and manufacturing method thereof Download PDFInfo
- Publication number
- KR20230014992A KR20230014992A KR1020210096215A KR20210096215A KR20230014992A KR 20230014992 A KR20230014992 A KR 20230014992A KR 1020210096215 A KR1020210096215 A KR 1020210096215A KR 20210096215 A KR20210096215 A KR 20210096215A KR 20230014992 A KR20230014992 A KR 20230014992A
- Authority
- KR
- South Korea
- Prior art keywords
- fertilizer
- matrix
- weight
- component
- slow release
- Prior art date
Links
- 239000003337 fertilizer Substances 0.000 title claims abstract description 91
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 20
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims abstract description 18
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 claims abstract description 18
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 claims abstract description 18
- 229920005989 resin Polymers 0.000 claims abstract description 17
- 239000011347 resin Substances 0.000 claims abstract description 17
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000004202 carbamide Substances 0.000 claims abstract description 10
- 239000011159 matrix material Substances 0.000 claims abstract description 8
- 239000000203 mixture Substances 0.000 claims abstract description 8
- 229920006167 biodegradable resin Polymers 0.000 claims abstract description 7
- 238000002156 mixing Methods 0.000 claims abstract description 7
- 229920001610 polycaprolactone Polymers 0.000 claims abstract description 4
- 239000004632 polycaprolactone Substances 0.000 claims abstract description 4
- 238000000576 coating method Methods 0.000 claims description 23
- 239000011248 coating agent Substances 0.000 claims description 20
- 238000000034 method Methods 0.000 claims description 18
- 239000002245 particle Substances 0.000 claims description 13
- 239000002274 desiccant Substances 0.000 claims description 5
- 239000000057 synthetic resin Substances 0.000 claims description 5
- 229920003002 synthetic resin Polymers 0.000 claims description 5
- 239000008187 granular material Substances 0.000 claims description 4
- 235000021355 Stearic acid Nutrition 0.000 claims description 3
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 3
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 claims description 3
- 239000008117 stearic acid Substances 0.000 claims description 3
- 229920001187 thermosetting polymer Polymers 0.000 claims description 3
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical group [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims description 2
- 239000001110 calcium chloride Substances 0.000 claims description 2
- 229910001628 calcium chloride Inorganic materials 0.000 claims description 2
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims description 2
- 239000000292 calcium oxide Substances 0.000 claims description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims description 2
- 239000003895 organic fertilizer Substances 0.000 claims description 2
- 239000002686 phosphate fertilizer Substances 0.000 claims description 2
- 229920005992 thermoplastic resin Polymers 0.000 claims description 2
- IPCSVZSSVZVIGE-UHFFFAOYSA-N hexadecanoic acid Chemical compound CCCCCCCCCCCCCCCC(O)=O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 claims 2
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 claims 1
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 claims 1
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 claims 1
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 claims 1
- 239000005642 Oleic acid Substances 0.000 claims 1
- 235000021314 Palmitic acid Nutrition 0.000 claims 1
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 235000014113 dietary fatty acids Nutrition 0.000 claims 1
- 238000001125 extrusion Methods 0.000 claims 1
- 239000000194 fatty acid Substances 0.000 claims 1
- 229930195729 fatty acid Natural products 0.000 claims 1
- 150000004665 fatty acids Chemical group 0.000 claims 1
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 claims 1
- WQEPLUUGTLDZJY-UHFFFAOYSA-N n-Pentadecanoic acid Natural products CCCCCCCCCCCCCCC(O)=O WQEPLUUGTLDZJY-UHFFFAOYSA-N 0.000 claims 1
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 claims 1
- 235000021313 oleic acid Nutrition 0.000 claims 1
- 229940072033 potash Drugs 0.000 claims 1
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims 1
- 235000015320 potassium carbonate Nutrition 0.000 claims 1
- 239000003784 tall oil Substances 0.000 claims 1
- 239000002023 wood Substances 0.000 claims 1
- 238000002844 melting Methods 0.000 abstract description 4
- 230000008018 melting Effects 0.000 abstract description 4
- 239000001993 wax Substances 0.000 abstract 1
- 239000000463 material Substances 0.000 description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- 238000004090 dissolution Methods 0.000 description 10
- 239000000126 substance Substances 0.000 description 7
- 239000003960 organic solvent Substances 0.000 description 6
- 239000002689 soil Substances 0.000 description 6
- 239000012528 membrane Substances 0.000 description 5
- 230000004720 fertilization Effects 0.000 description 4
- 239000002861 polymer material Substances 0.000 description 4
- 238000011109 contamination Methods 0.000 description 3
- 238000010828 elution Methods 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerol Natural products OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- QFHMNFAUXJAINK-UHFFFAOYSA-N [1-(carbamoylamino)-2-methylpropyl]urea Chemical compound NC(=O)NC(C(C)C)NC(N)=O QFHMNFAUXJAINK-UHFFFAOYSA-N 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 244000037666 field crops Species 0.000 description 2
- 238000000053 physical method Methods 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 229920001059 synthetic polymer Polymers 0.000 description 2
- IHBLBMDDUQOYLA-UHFFFAOYSA-N 1-octadecyl-3-[4-[[4-(octadecylcarbamoylamino)phenyl]methyl]phenyl]urea Chemical compound C1=CC(NC(=O)NCCCCCCCCCCCCCCCCCC)=CC=C1CC1=CC=C(NC(=O)NCCCCCCCCCCCCCCCCCC)C=C1 IHBLBMDDUQOYLA-UHFFFAOYSA-N 0.000 description 1
- HECLRDQVFMWTQS-RGOKHQFPSA-N 1755-01-7 Chemical compound C1[C@H]2[C@@H]3CC=C[C@@H]3[C@@H]1C=C2 HECLRDQVFMWTQS-RGOKHQFPSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 229920001807 Urea-formaldehyde Polymers 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000001934 delay Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000007922 dissolution test Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 1
- -1 glycerol ester Chemical class 0.000 description 1
- 239000004816 latex Substances 0.000 description 1
- 229920000126 latex Polymers 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 230000003204 osmotic effect Effects 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- ODGAOXROABLFNM-UHFFFAOYSA-N polynoxylin Chemical compound O=C.NC(N)=O ODGAOXROABLFNM-UHFFFAOYSA-N 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000011253 protective coating Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000002195 soluble material Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G5/00—Fertilisers characterised by their form
- C05G5/40—Fertilisers incorporated into a matrix
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/60—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
- B01F27/72—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with helices or sections of helices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G1/00—Mixtures of fertilisers belonging individually to different subclasses of C05
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G3/00—Mixtures of one or more fertilisers with additives not having a specially fertilising activity
- C05G3/40—Mixtures of one or more fertilisers with additives not having a specially fertilising activity for affecting fertiliser dosage or release rate; for affecting solubility
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G3/00—Mixtures of one or more fertilisers with additives not having a specially fertilising activity
- C05G3/50—Surfactants; Emulsifiers
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G3/00—Mixtures of one or more fertilisers with additives not having a specially fertilising activity
- C05G3/70—Mixtures of one or more fertilisers with additives not having a specially fertilising activity for affecting wettability, e.g. drying agents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/005—Mixing or agitating manure, dung
Abstract
Description
본 발명은 생분해성 SAP와 수지 그리고 비료를 혼합한후 압출기를 통하여 압출시켜 매트릭스수지로 비료성분을 피복시킴으로서 비료성분과 수분의 제공을 지속적으로 할 수 있도록 한 경제성이 높고 환경친화적인 새로운 형태의 매트릭스형 환효성 및 그의 제조방법에 관한 것이다.The present invention mixes biodegradable SAP, resin, and fertilizer and then extrudes them through an extruder to coat the fertilizer components with the matrix resin, which is a highly economical and environmentally friendly new type of matrix that enables continuous provision of fertilizer components and moisture. It relates to the mold conversion effect and its preparation method.
종래의 완효성 비료의 제조방법에는, 비료성분을 다른 물질과 화학적으로 반응시켜 물에 난용성인 염이나 토양미생물에 의해 쉽게 분해되지 않는 난분해성 물질로 변화시켜 비료성분의 용해도 자체를 감소시키는 화학적 방법과, 속효성 비료의 입자표면에 물의 접촉을 차단할 수 있는 난용성 물질로 피복하여 비료성분 의 용출속도를 늦추는 물리적 방법이 있다. 화학적 방법으로 만든 제품에는 요소와 알데히드를 축합시킨 Urea-Formaldehyde,IBDU(Isobuty lidene Diureas), CDU 등의 제품이 나와 있으나(미국 특허 제3,227,543호), 이 제품은 그 제조공정이 화학적 합성에 의하여 제조되므로 공정이 복잡하고 생산원가가 비싸다는 단점이 있다. 물리적 방법은 화학적 방법과는 달리 속효성 비료의 입자표면을 피복하여 비료의 용출률을 조절하는 것으로, 피복물질의 종류에 따라 적은 양의 피복물질로 충분한 지속성 효과를 얻을 수 있고, 용출속도의 조절이 용이하여, 화학적 방법보다는 제조공정이 간단하다는 이점이 있어 이 방면에서 연구와 개발이 활발히 진행되고 있다. 비료입자의 표면에 피복된 피복막의 종류에는 확산에 의해 생긴 내부삼투압으로 막이 파괴되어 비료성분이 용출되는 반투수성막(열가소성 합성수지), 물이 막을 통과하여 내부로 들어가서 비료성분을 녹이고 구멍을 크게하여 비료성분을 용출시키는 미세구멍이 있는 불투수성막(열경화성 합성수지), 물리화학적 또는 미생물의 활동에 의하여 피복물질을 분해시켜 비료성분이 용출되는 불투수성막(생분해수지)등이 있다. 피복물질로 이용될 수 있는 물질에는 합성수지물질 및 생분해물질이 있으며, 합성수지 물질에는 다시 열경화성수지와 열가소성수지가 있다. 지금까지의 피복형 비료는 비료입자 개개를 피복물질로 피복시킨 것으로서 대표적인 것을 살펴보면 아래와 같다. 미국의 아쿼-다니엘스-미들랜드 컴퍼니(Archer Daniels Midland Company)에서 개발한 오스모코트(Osmocote)(미국 특허 제3,233,518호)는 Dicyclopentadien e와 glycerol ester의 공중합체를 피복물질로 하여 다층 피복한 것으로 품질은 우수하나 제품의 가격이 비싸고 사용한 유기용매의 회수가 어려워 환경오염의 우려가 높다. 미국의 T.V.A사에서 개발한 유황피복비료(미국 특허 제3,295,950호)는 제품가격은 저렴하나 비료의 용출속도 조절이 어렵고 축적된 유황으로 토양이 산성화되는 문제가 있다. 그외에 금속산화물인 규산염을 사용한 경우(일본 특허 제59,137,386호)가 있으나 피복물질인 규산염이 물에 용해되어 피복막의 성능이 오래가지 않는 단점이 있어서, 그후 보완되어 규산염을 피복후 고분자 라텍스로 이중 피복하여 수중에서 비료성분의 용출을 지연시킨(대한민국 특허공고 제88-153) 방법이 있으나, 이 역시 제조비용이 높은 단점과 라텍스 성분이 토양에 잔류축적되는 문제가 있다. 상기한 바와 같이 합성구분자 물질을 사용하여 비료성분을 피복시키는 방법에서는 합성고분자물질에 의한 토양오염 등의 문제가 있어서, 합성고분자물질 이외에 생분해 물질을 사용하는 것이 제안되었다. 생분해물질로 물에 녹지 않는 왁스를 사용(미국 특허 제3,232,237호) 하였으나 왁스를 사용하는 경우 비료의 용출속도를 만족할 만큼 억제시키기 위해서는 피복재료인 왁스 함량이 너무 높아지게 되는 단점이 있다. 이를 보완하기 위해 옥스와 로진을 혼합용융하여 피복재료로 이용하는 방법(일본 특허 공고 제59-35875호)이 제안되었다. 그러나 로진을 피복재로로 사용하는 경우 피복재료를 용매에 용해시킨 후 비료입자에 분무하여 피막을 형성시키는 과정에서 고열에 의한 로진의 분해로 피복막에 극심한 핀홀이 생긴다는 문제점이 대두되었다. 생분해물질을 이용하여 피막을 수해아는 과정에서 발생하는 사이 핀홀현상을 제거하기 위해 로진을 유기용매에 용해시킨 후 특정 첨가제를 가해 입상비료의 피복물질로 사용(대한민국 특허공개 93-12646)하는방법이 제안되었다. 이 방법은 낮은 온도에서 피막공정을 수행할 수 있게 함으로써 로진피막의 핀홀 발생을 억제하여 로진피막의 물성을 개선하여 완효성을 놓게한 것이다. 그러나, 이 경우에는 입자표면의 점성으로 인하여 저장 및 취급시에 입자끼지 엉겨붙거나 서로 부딪쳐 마모되는 경향이 있으므로, 이를 보완하여 로진 및 로진 유도체 혼합물에 고분자물질을 첨가한 후 유기용매에 용해하여 입상비료에 분무 피복후 유기 고분자 물질을 유기용액 또는 에멀젼용액 형태로 보호피복 시키는(대한민국 특허공개 제94-2203호) 완효성 비료의 제조방법이 제안되었다. 이 방밥으로 피복된 입자는 기계적 강도가 증가되어 취급 및 저장시 발생하는 문제는 해결되었으나, 제조공정이 복잡하고 유기용매 사용으로 인한 문제가 발생하였다.In the conventional manufacturing method of slow-acting fertilizer, a chemical method of reducing the solubility of the fertilizer component itself by chemically reacting the fertilizer component with other substances to change it into a salt that is poorly soluble in water or a non-degradable substance that is not easily decomposed by soil microorganisms, and In other words, there is a physical method of slowing down the dissolution rate of fertilizer components by coating the particle surface of the quick-acting fertilizer with a poorly soluble material that can block contact with water. Products made by chemical methods include Urea-Formaldehyde, IBDU (Isobuty lidene Diureas), and CDU, which are condensed with urea and aldehyde (U.S. Patent No. 3,227,543), but these products are manufactured by chemical synthesis. Therefore, the process is complicated and the production cost is high. Unlike the chemical method, the physical method controls the dissolution rate of the fertilizer by coating the particle surface of the quick-acting fertilizer. Therefore, there is an advantage in that the manufacturing process is simpler than the chemical method, so research and development are being actively conducted in this area. The types of coatings coated on the surface of fertilizer particles include a semi-permeable membrane (thermoplastic synthetic resin) in which the membrane is destroyed by the internal osmotic pressure generated by diffusion and the fertilizer components are eluted, and water passes through the membrane and enters the inside to dissolve the fertilizer components and enlarge the hole. There are impermeable membranes (thermosetting synthetic resins) with micropores that elute fertilizer components, and impervious membranes (biodegradable resins) that elute fertilizer components by decomposing coating materials by physicochemical or microbial activity. Materials that can be used as coating materials include synthetic resin materials and biodegradable materials, and synthetic resin materials include thermosetting resins and thermoplastic resins. Until now, coating fertilizers are those in which individual fertilizer particles are coated with a coating material, and representative examples are as follows. Osmocote (U.S. Patent No. 3,233,518), developed by Archer Daniels Midland Company in the United States, is a multi-layered coating made of a copolymer of dicyclopentadiene and glycerol ester. It is excellent, but the product is expensive and it is difficult to recover used organic solvents, so there is a high concern about environmental pollution. Sulfur-coated fertilizer (US Patent No. 3,295,950) developed by T.V.A of the United States has a low product price, but it is difficult to control the dissolution rate of the fertilizer and has a problem of acidification of the soil due to accumulated sulfur. In addition, there is a case in which silicate, which is a metal oxide, is used (Japanese Patent No. 59,137,386), but the coating material, silicate, dissolves in water and the performance of the coating film does not last long. There is a method that delays the dissolution of fertilizer components in water (Korean Patent Publication No. 88-153), but this also has the disadvantage of high manufacturing cost and the problem of residual accumulation of latex components in the soil. As described above, in the method of coating fertilizer components using synthetic separator materials, there is a problem such as soil contamination by synthetic polymer materials, so it is proposed to use biodegradable materials in addition to synthetic polymer materials. Wax insoluble in water was used as a biodegradable material (U.S. Patent No. 3,232,237). However, in the case of using wax, the wax content of the coating material is too high in order to satisfactorily suppress the dissolution rate of the fertilizer. To compensate for this, a method of mixing and melting ox and rosin and using them as a coating material (Japanese Patent Publication No. 59-35875) has been proposed. However, when rosin is used as a coating material, the coating material is dissolved in a solvent and then sprayed on fertilizer particles to form a film. In the process of forming a film, rosin is decomposed by high heat, resulting in extreme pinholes in the film. In order to eliminate the pinhole phenomenon that occurs during the process of watering the film using biodegradable materials, rosin is dissolved in an organic solvent and then a specific additive is added to use it as a coating material for granular fertilizer (Korean Patent Publication No. 93-12646). has been suggested This method allows the coating process to be performed at a low temperature, thereby suppressing the occurrence of pinholes in the rosin coating and improving the physical properties of the rosin coating to increase the effectiveness. However, in this case, due to the viscosity of the surface of the particles, the particles tend to stick together or collide with each other during storage and handling, so to compensate for this, a polymer material is added to the mixture of rosin and rosin derivatives, and then dissolved in an organic solvent to form granular A method for producing a slow release fertilizer has been proposed in which the organic polymer material is coated with a protective coating in the form of an organic solution or an emulsion solution after spraying the fertilizer (Korean Patent Publication No. 94-2203). The particles coated with this method have increased mechanical strength, which solves problems during handling and storage, but the manufacturing process is complicated and problems arise due to the use of organic solvents.
현재 사용되고 있는 화학비료는 대부분 물에 녹기 때문에 시비 직후 비료가 과다 용출되고, 시비된 비료의 유실량이 많아 비료의 이용율이 떨어지며, 비료의 유실에 따른 과다한 시비로 토양중의 염의 축적에 의한 환경오염 및 빈번한 시비에 의한 노동력 낭비 등의 문제점이 있다. 따라서 시비된 비료의 유실량을 줄이고, 빈번한 시비에 따른 노동력을 절감하고 작물의전 생육기간에 걸쳐 비료성분을 지속적으로 공급해줄 수 있는 완효성 비료의 개발이 절실히 요구되고 있는 실정이다. 또한 수분의 제공에 있어서도 지속성이 떨어져 자주 물을 공급해야하는 어려움이 있어, 수분과 비료의 공급 문제를 동시에 해결하고, 토양의 오염을 최소화 할 수 있는 생분해성 SAP를 이용한 완효성 비료의 개발이 특히 밭작물에 있어 더욱 절실하게 필요한 실정이다.Since most of the currently used chemical fertilizers are soluble in water, the fertilizer is excessively eluted immediately after fertilization, and the amount of loss of the fertilized fertilizer is large, resulting in a decrease in the utilization rate of fertilizer. There are problems such as waste of labor due to frequent fertilization. Therefore, there is an urgent need to develop a slow-acting fertilizer that can reduce the loss of fertilized fertilizer, reduce labor force due to frequent fertilization, and continuously supply fertilizer components throughout the entire growth period of crops. In addition, there is a difficulty in supplying water frequently due to poor sustainability in providing moisture, so the development of a slow-acting fertilizer using biodegradable SAP that can solve the problem of supplying water and fertilizer at the same time and minimize soil contamination is particularly important for field crops. It is more urgently needed.
본 발명은 상기한 바와 같은 문제점을 해결하기 위하여 안출된 것으로서, 기존의 피복비료와는 전혀 다른 새로운 피복방법으로 제조되는 매트릭스형 완효성 비료 및 그의 제조방법을 제공함에 그 목적이 있다. 또한 생분해성SAP를 혼합하여 수분의 제공이 동시에 이루어질 수 있도록 제조한 특성을 갖고 있다. 상기한 바와 같은 목적을 달성하기 위한 본 발명에 따른 매트릭스형 완효성 비료는 5-80중량%의 SAP성분 입상체(粒狀體)와 5-80중량%의 수지성분 입상체(粒狀體)에 20-95중량%의 비료입자가 산포되어 존재되도록 형성된 것을 특징으로 한다. 또한, 본 발명에 따른 매트릭스형 완효성 비료의 제조방법은 SAP성분 5-80중량%, 수지성분 5-80중량%, 비료성분 20-95중량%, 필요하면 표면상용화제 0-20중량%, 건조제 0-20중량%로 구성되는 혼합물을 압출기내에서 용융혼합을 한후 압축시켜 비료성분을 매트릭스수지로 피복시키는 것을 특징으로 한다. 상기한 바와 같은 제조방법으로 제조되는 매트릭스형 완효성 비료는 SAP와 수지성분으로 된 매트릭스형 입체상에 비료입자가 산포된 상태이므로 상기 수지의 중량비를 조절함에 의해 비료성분의 수중 용출속도의 조절이 용이하게 이루어질 수 있으며, 아울러 소량의 피복물질(수지)로 다량의 비료성분을 피복할 수 있어 환경오염을 최소화할 수 있고, 유기용매를 사용하지 않으므로 용매의 회수 문제가 발생하지 않으며, 공정이 간단한 이점이 있다.The present invention has been made to solve the above problems, and an object of the present invention is to provide a matrix-type slow release fertilizer and a manufacturing method thereof produced by a completely different coating method from existing coated fertilizers. In addition, it has the characteristics of being manufactured so that water can be provided at the same time by mixing biodegradable SAP. Matrix type slow release fertilizer according to the present invention for achieving the above object is 5-80% by weight of SAP component granules and 5-80% by weight of resin component granules It is characterized in that it is formed so that 20-95% by weight of fertilizer particles are dispersed and present. In addition, the method for producing a matrix-type slow-release fertilizer according to the present invention includes 5-80% by weight of SAP component, 5-80% by weight of resin component, 20-95% by weight of fertilizer component, 0-20% by weight of surface compatibilizer if necessary, desiccant It is characterized in that the mixture composed of 0-20% by weight is melt-mixed in an extruder and then compressed to coat the fertilizer component with a matrix resin. Since the matrix-type slow-release fertilizer produced by the manufacturing method as described above is a state in which fertilizer particles are dispersed in a matrix-type three-dimensional phase composed of SAP and resin components, it is easy to control the dissolution rate of fertilizer components in water by adjusting the weight ratio of the resin. In addition, since a large amount of fertilizer components can be coated with a small amount of coating material (resin), environmental pollution can be minimized, and since organic solvents are not used, solvent recovery problems do not occur, and the process is simple. there is
본 발명의 제조방법에 의해 제조되는 매트릭스형 완효성 비료는 생분해성 SAP와 수지를 사용하고 특정 첨가물이나 유기용매를 전혀 사용하지 않음으로서 환경 및 토양오염의 문제를 해결하였다. 또한 생분해성 수지 즉 로진이나 왁스, Polycaprolactone 등과 유사한 융점을 가진 수지들은 모두 이용 가능하여 기존의 분무 피복시 사용되는 원료를 사용할 수 있으므로 원료선택의 폭이 넓고, 이들을 분쇄된 형태 또는 그대로 용도에 따라 적정 중량%로 비료에 혼합시켜 수퍼믹스, 니더 혹은 반바리에 넣어 혼합시킨 후 압출기에 넣어줌으로 별도의 전처리 과정이 필요하지 않아 제조공정이 간단해짐으로 제조원가를 절감할 수 있으며, 이에 따라 대량 생산이 가능하고, 요소질 비료를 비롯하여 인산질, 칼리질 및 유기질 비료를 그 대상으로 할 수있어 다양한 용도의 완효성 비료를 제조할 수 있다. 또한 생분해성SAP, 생분해성수지(로진, 왁스 Polycaprolactone 또는 각각의 혼합물)와 비료(요소비료, 인사질비료, 칼리질비료, 유기질비료, 또는 복합비료)를 혼합시킬때 건조제(염화칼슘, 산화칼슘)를 첨거하여 혼합시킨 후 압출기를 통해 피복시킨 비료는, 용융혼합시 수분증발에 따라 생성되는 기공의 발생을 줄여줌으로 피복층이 단단해져 물의침투를 막아줌으로, 흡습성이 있는 요소비료 입자의 경우 더 좋은 완효성을 나타나게 된다. 표면 상용화제를 넣은 경우에는, 비료입자의 친수성과 생분해성 수지의 소수성 사이의 접착력을 증가시킴으로 강도 높은 압축펠렛을 얻을 수있으므로, 피복비료의 강도를 증가시켜서 운반저장 및 시비후 용출량을 조절하기 쉽다. 또한, 단축압출기를 통과시켜 얻은 펠렛에 비해 이축압출기를 통과시키거나 이축압출기를 통과시킨후 다시 단축압출기로 압출되어 나온 펠렛은 기계적 강도와 완효성이 증가되어, 비료의 용출기간이 길게 필요한 밭작물에 적용이 가능하다.The matrix-type slow-release fertilizer prepared by the manufacturing method of the present invention uses biodegradable SAP and resin and solves the problem of environmental and soil contamination by not using specific additives or organic solvents at all. In addition, since biodegradable resins, such as rosin, wax, and polycaprolactone, which have similar melting points, are all available, raw materials used in conventional spray coating can be used, so the range of raw material selection is wide, and they can be appropriated according to the application in the form of pulverized or as is. It is mixed with fertilizer by weight %, mixed in a super mix, kneader or banbari, and then put into an extruder, which simplifies the manufacturing process because no pretreatment process is required, thereby reducing manufacturing costs, and thus mass production is possible. It is possible, and phosphate, potassium, and organic fertilizers as well as urea fertilizers can be used to manufacture slow-acting fertilizers for various purposes. In addition, when mixing biodegradable SAP, biodegradable resin (rosin, wax polycaprolactone, or each mixture) and fertilizer (urea fertilizer, phosphate fertilizer, potassium fertilizer, organic fertilizer, or compound fertilizer), desiccant (calcium chloride, calcium oxide) Fertilizer coated through an extruder after adding and mixing the fertilizer reduces the occurrence of pores generated by water evaporation during melting and mixing, and the coating layer becomes hard to prevent water penetration, so in the case of hygroscopic urea fertilizer particles, better efficiency will appear. When the surface compatibilizer is added, it is possible to obtain high-strength compressed pellets by increasing the adhesive force between the hydrophilicity of the fertilizer particles and the hydrophobicity of the biodegradable resin, so it is easy to control the elution amount after transportation, storage and fertilization by increasing the strength of the coated fertilizer. . In addition, compared to pellets obtained by passing through a single-screw extruder, pellets passed through a twin-screw extruder or extruded through a twin-screw extruder and then extruded through a single-screw extruder have increased mechanical strength and effectiveness, and are applied to field crops that require a long period of fertilizer elution. this is possible
제1도(a)는 본 발명의 제조방법에 의해 피복된 매트리스형 완효성 비료의 단면도
제1도(b)는 기존의 분무피복방법에 의해 피복된 비료의 단면도Figure 1 (a) is a cross-sectional view of the mattress-type slow release fertilizer coated by the manufacturing method of the present invention
Figure 1 (b) is a cross-sectional view of the fertilizer coated by the conventional spray coating method
본 발명을 실시예를 들어 더욱 구체적으로 설명하면 다음과 같다.The present invention will be described in more detail with examples as follows.
이들 실시예는 본원 발명의 일부를 보여주는 것으로서 본 실시예들에 의해 본 발명의 범위가 제한되는 것은 아니다. These examples show a part of the present invention, and the scope of the present invention is not limited by these examples.
[실시예 1][Example 1]
본 실시예는 제조공정의 특징을 나타낸 것으로 일반시판되고 있는 입자형 요소비료 2.5kg과, SAP 2.5kg, 분쇄한 검로진 4kg에 왁스 1kg을, 스크류의 회전속도는 100rpm, 온도 60-110℃로 조작된 단축압출기에 투입한다. 압출기 다이를 통과한 피복비료를 일정한 크기로 절단하여 완효성 실험을 실시한 결과 다음의 표 1과 같이 나타났다. 용출실험은 30℃ 항온조에서 용출되는 비료의 양을 측정하여 결과를 얻었다. This example shows the characteristics of the manufacturing process. 2.5 kg of commercially available particulate urea fertilizer, 2.5 kg of SAP, 4 kg of pulverized gum rosin, 1 kg of wax, screw rotation speed of 100 rpm, temperature of 60-110 ° C. It is put into the operated single-screw extruder. The coated fertilizer passed through the extruder die was cut into a certain size and the effectivity test was conducted, and the results were shown in Table 1 below. The dissolution test obtained the result by measuring the amount of fertilizer eluted from the 30 ℃ thermostat.
[실시예 2][Example 2]
일반 시판되고 있는 입자형 요소비료 3.5kg과, SAP 3.5kg, 분쇄한 검로진 3kg을 수퍼믹스에 넣고 혼합한다. 혼합된 물질을 이축압출기에 투입하는데, 이때 압출기내의 온도는 80-120℃로, 스크류의 회전속도는 200rpm을 유지한다. 실시예1과 같은 방법으로 완효성 실험을 실시한 결과 다음의 표 2와 같이 나타났다.3.5 kg of commercially available granular urea fertilizer, 3.5 kg of SAP, and 3 kg of pulverized gum rosin were added to the supermix and mixed. The mixed material is put into a twin-screw extruder, where the temperature in the extruder is maintained at 80-120° C. and the rotational speed of the screw is 200 rpm. As a result of conducting the efficacy test in the same manner as in Example 1, the results were shown in Table 2 below.
[실시예 3][Example 3]
일반 시판되고 있는 입자형 요소비료 3.5kg과, SAP 3.5kg, 분쇄한 검로진 2.5kg을 스테아린산 0.5kg을 슈퍼믹스에 넣고 혼합한다. 혼합된 물질을 이축압출기에 투입하는데, 이때 압출기내의 온도는 80-120℃로, 스크류의 회전속도는 200rpm을 유지한다. 이축 압출기 다이를 통과한 혼합물이 다시 단축압출기로 투입되도록 하는데, 이때 단축압출기 내의 온도는 60-120℃로 조작되고, 스크류의 회전속도는 150rpm을 유지시킨다. 실시예 1과 같은 방법으로 완효성 실험을 실시한 결과 다음의 표 3과 같이 나타났다.3.5 kg of commercially available granular urea fertilizer, 3.5 kg of SAP, and 2.5 kg of pulverized gum rosin were mixed with 0.5 kg of stearic acid in a supermix. The mixed material is put into a twin-screw extruder, where the temperature in the extruder is maintained at 80-120° C. and the rotational speed of the screw is 200 rpm. The mixture passing through the die of the twin-screw extruder is put into the single-screw extruder again. At this time, the temperature in the single-screw extruder is operated at 60-120 ° C., and the rotational speed of the screw is maintained at 150 rpm. As a result of conducting the efficacy test in the same manner as in Example 1, the results are shown in Table 3 below.
[실예 4][Example 4]
일반 시판되고 있는 입자형 요소비료 4kg에 SAP 4kg, 검로진 1.7kg과 스테아린산 0.3kg을 넣어 120℃로 예열된 반바리에 넣고 5분간 혼합한 후, 실시예 1과 같은 방법으로 혼합피복으로 용출시험을 실시한 결과 다음의 표 4와 같이 나타났다.Put 4 kg of SAP, 1.7 kg of gum rosin, and 0.3 kg of stearic acid into 4 kg of commercially available granular urea fertilizer, put them in a preheated banbari at 120 ° C, mix for 5 minutes, and then test the elution with mixed coating in the same manner as in Example 1. The result was shown in Table 4 below.
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